JP2000319667A - 触媒の金属許容性を増加させる改良された残油流動接触分解方法 - Google Patents
触媒の金属許容性を増加させる改良された残油流動接触分解方法Info
- Publication number
- JP2000319667A JP2000319667A JP2000113255A JP2000113255A JP2000319667A JP 2000319667 A JP2000319667 A JP 2000319667A JP 2000113255 A JP2000113255 A JP 2000113255A JP 2000113255 A JP2000113255 A JP 2000113255A JP 2000319667 A JP2000319667 A JP 2000319667A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- catalytic cracking
- fluid catalytic
- regeneration
- resid
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims abstract description 57
- 238000004231 fluid catalytic cracking Methods 0.000 title claims abstract description 52
- 230000008569 process Effects 0.000 title claims abstract description 45
- 229910052751 metal Inorganic materials 0.000 title description 25
- 239000002184 metal Substances 0.000 title description 25
- 230000003197 catalytic effect Effects 0.000 title description 9
- 239000003054 catalyst Substances 0.000 claims abstract description 148
- 229910052720 vanadium Inorganic materials 0.000 claims abstract description 37
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 claims abstract description 37
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims abstract description 32
- 229910052708 sodium Inorganic materials 0.000 claims abstract description 32
- 239000011734 sodium Substances 0.000 claims abstract description 32
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 20
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 20
- 239000001301 oxygen Substances 0.000 claims abstract description 20
- 239000007789 gas Substances 0.000 claims abstract description 14
- 230000001172 regenerating effect Effects 0.000 claims abstract description 7
- 238000002485 combustion reaction Methods 0.000 claims description 23
- 238000011069 regeneration method Methods 0.000 claims description 23
- 230000008929 regeneration Effects 0.000 claims description 21
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 19
- 229910052799 carbon Inorganic materials 0.000 claims description 19
- 230000009849 deactivation Effects 0.000 claims description 17
- 239000003546 flue gas Substances 0.000 claims description 17
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 16
- 229930195733 hydrocarbon Natural products 0.000 claims description 15
- 150000002430 hydrocarbons Chemical class 0.000 claims description 15
- 239000004215 Carbon black (E152) Substances 0.000 claims description 14
- 230000003647 oxidation Effects 0.000 claims description 9
- 238000007254 oxidation reaction Methods 0.000 claims description 9
- 238000005336 cracking Methods 0.000 claims description 7
- 239000000567 combustion gas Substances 0.000 claims description 2
- 230000002779 inactivation Effects 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 12
- 230000000694 effects Effects 0.000 description 11
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 10
- 229910052717 sulfur Inorganic materials 0.000 description 10
- 239000011593 sulfur Substances 0.000 description 10
- 150000002739 metals Chemical class 0.000 description 9
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 239000000446 fuel Substances 0.000 description 7
- 239000002574 poison Substances 0.000 description 7
- 231100000614 poison Toxicity 0.000 description 7
- 239000000571 coke Substances 0.000 description 6
- 239000010779 crude oil Substances 0.000 description 5
- 238000013461 design Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 230000001590 oxidative effect Effects 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 4
- 230000007246 mechanism Effects 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 229910021536 Zeolite Inorganic materials 0.000 description 3
- 230000033228 biological regulation Effects 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000010457 zeolite Substances 0.000 description 3
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000004523 catalytic cracking Methods 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- GNTDGMZSJNCJKK-UHFFFAOYSA-N divanadium pentaoxide Chemical compound O=[V](=O)O[V](=O)=O GNTDGMZSJNCJKK-UHFFFAOYSA-N 0.000 description 2
- 239000003502 gasoline Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 238000005504 petroleum refining Methods 0.000 description 2
- 239000002243 precursor Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- WQEVDHBJGNOKKO-UHFFFAOYSA-K vanadic acid Chemical compound O[V](O)(O)=O WQEVDHBJGNOKKO-UHFFFAOYSA-K 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000001934 delay Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 230000001665 lethal effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000006902 nitrogenation reaction Methods 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 150000002902 organometallic compounds Chemical class 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 230000003134 recirculating effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 150000003388 sodium compounds Chemical class 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 150000004763 sulfides Chemical class 0.000 description 1
- 150000003464 sulfur compounds Chemical class 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 229910052815 sulfur oxide Inorganic materials 0.000 description 1
- LSGOVYNHVSXFFJ-UHFFFAOYSA-N vanadate(3-) Chemical compound [O-][V]([O-])([O-])=O LSGOVYNHVSXFFJ-UHFFFAOYSA-N 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
- C10G11/182—Regeneration
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US28866599A | 1999-04-09 | 1999-04-09 | |
| US09/288665 | 1999-04-09 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000319667A true JP2000319667A (ja) | 2000-11-21 |
Family
ID=23108106
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000113255A Pending JP2000319667A (ja) | 1999-04-09 | 2000-04-10 | 触媒の金属許容性を増加させる改良された残油流動接触分解方法 |
Country Status (2)
| Country | Link |
|---|---|
| EP (1) | EP1043384A3 (de) |
| JP (1) | JP2000319667A (de) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011137154A (ja) * | 2009-12-28 | 2011-07-14 | Petroleo Brasileiro Sa | 二酸化炭素の排出を低減させた流動接触分解法 |
| JP2020169235A (ja) * | 2019-04-01 | 2020-10-15 | 出光興産株式会社 | 流動接触分解ガソリンの製造方法 |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20030075480A1 (en) * | 2001-10-24 | 2003-04-24 | Barco Processes Joint Venture | Process for controlling oxidation of nitrogen and metals in circulating fluidized solids contacting process |
| CN1333044C (zh) * | 2003-09-28 | 2007-08-22 | 中国石油化工股份有限公司 | 一种烃油裂化方法 |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4377470A (en) * | 1981-04-20 | 1983-03-22 | Ashland Oil, Inc. | Immobilization of vanadia deposited on catalytic materials during carbo-metallic oil conversion |
| CA1242985A (en) * | 1984-02-08 | 1988-10-11 | William P. Hegarty | Method for controlling fluidized catalytic cracker regenerator temperature and velocity with carbon dioxide |
| US5077252A (en) * | 1990-07-17 | 1991-12-31 | Mobil Oil Corporation | Process for control of multistage catalyst regeneration with partial co combustion |
| FR2675714B1 (fr) * | 1991-04-26 | 1993-07-16 | Inst Francais Du Petrole | Procede et dispositif d'echange thermique de particules solides pour regeneration en craquage catalytique. |
| US5584986A (en) * | 1993-03-19 | 1996-12-17 | Bar-Co Processes Joint Venture | Fluidized process for improved stripping and/or cooling of particulate spent solids, and reduction of sulfur oxide emissions |
| EP0724009A1 (de) * | 1995-01-30 | 1996-07-31 | Exxon Research And Engineering Company | Katalytischer Krackverfahren und Vorrichtung dazu |
| US5716514A (en) * | 1995-08-30 | 1998-02-10 | Mobil Oil Corporation | FCC NOx reduction by turbulent/laminar thermal conversion |
| US5827793A (en) * | 1996-04-11 | 1998-10-27 | Exxon Research And Engineering Company | Controlled FCC catalyst regeneration using a distributed air system |
-
2000
- 2000-04-06 EP EP00610038A patent/EP1043384A3/de not_active Withdrawn
- 2000-04-10 JP JP2000113255A patent/JP2000319667A/ja active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2011137154A (ja) * | 2009-12-28 | 2011-07-14 | Petroleo Brasileiro Sa | 二酸化炭素の排出を低減させた流動接触分解法 |
| JP2020169235A (ja) * | 2019-04-01 | 2020-10-15 | 出光興産株式会社 | 流動接触分解ガソリンの製造方法 |
| JP7108570B2 (ja) | 2019-04-01 | 2022-07-28 | 出光興産株式会社 | 流動接触分解ガソリンの製造方法 |
Also Published As
| Publication number | Publication date |
|---|---|
| EP1043384A2 (de) | 2000-10-11 |
| EP1043384A3 (de) | 2001-05-30 |
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